CAPE-OPENDiscussions about CAPE-OPEN standards2019-03-12T14:00:38+00:00http://cape-open-forum.org/feed.php2019-03-12T14:00:38+00:002019-03-12T14:00:38+00:00http://cape-open-forum.org/viewtopic.php?t=659&p=2261#p2261The result at 25C and 1atm is a vapor and a liquid - the middle stream does not have any content on it (zero flow rate). Flash ROUT at 25C and you will see the same.

]]>2019-03-12T05:16:07+00:002019-03-12T05:16:07+00:00http://cape-open-forum.org/viewtopic.php?t=659&p=2260#p2260Statistics: Posted by aken — 12 March 2019, 05:16
]]>2019-03-11T10:14:19+00:002019-03-11T10:14:19+00:00http://cape-open-forum.org/viewtopic.php?t=658&p=2259#p2259On the 'Access Unit Operations' and 'Access Streams' example sheets you will find the corresponding formulae. You can change these at will by inspecting the VBA code.

]]>2019-02-17T09:37:33+00:002019-02-17T09:37:33+00:00http://cape-open-forum.org/viewtopic.php?t=655&p=2253#p2253Either re-install (and choose yes in case it is asking to register for CAPE-OPEN interop), or use register.bat in the bin folder of the ChemSep installation folder to re-register the CAPE-OPEN binaries for interop.

]]>2019-02-12T08:20:13+00:002019-02-12T08:20:13+00:00http://cape-open-forum.org/viewtopic.php?t=657&p=2250#p2250If you would want to use that in a flowsheet it becomes slightly more complicated as you would need a 1000 of those reactors. If pressure drop is negligible you could of course just multiply the heat transfer coefficient by 1000 to simulate that case.

]]>2019-02-12T00:49:21+00:002019-02-12T00:49:21+00:00http://cape-open-forum.org/viewtopic.php?t=656&p=2248#p2248Statistics: Posted by aken — 12 February 2019, 00:49
]]>2019-02-08T10:42:27+00:002019-02-08T10:42:27+00:00http://cape-open-forum.org/viewtopic.php?t=655&p=2247#p2247- download the new ChemSep- edit the unit to remove the Bottoms Flowrate input variable- then edit the unit again to add the Bottoms Flowrate input variable; now it will have units